EP0646396B1 - Balles de jeu, balles de tennis sans pression et compositions de caoutchouc pour les fabriques - Google Patents

Balles de jeu, balles de tennis sans pression et compositions de caoutchouc pour les fabriques Download PDF

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Publication number
EP0646396B1
EP0646396B1 EP94305731A EP94305731A EP0646396B1 EP 0646396 B1 EP0646396 B1 EP 0646396B1 EP 94305731 A EP94305731 A EP 94305731A EP 94305731 A EP94305731 A EP 94305731A EP 0646396 B1 EP0646396 B1 EP 0646396B1
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EP
European Patent Office
Prior art keywords
playball
ball
cellulose
polyethylene
phr
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EP94305731A
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German (de)
English (en)
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EP0646396A2 (fr
EP0646396A3 (fr
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Glen I. Hargis
Richard A. Miranda
John A. Wilson
Oon-Hock Yeoh
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Aerojet Rocketdyne Holdings Inc
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Gencorp Inc
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    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L7/00—Compositions of natural rubber
    • A—HUMAN NECESSITIES
    • A63—SPORTS; GAMES; AMUSEMENTS
    • A63B—APPARATUS FOR PHYSICAL TRAINING, GYMNASTICS, SWIMMING, CLIMBING, OR FENCING; BALL GAMES; TRAINING EQUIPMENT
    • A63B39/00—Hollow non-inflatable balls, i.e. having no valves
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L21/00—Compositions of unspecified rubbers
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K3/00—Use of inorganic substances as compounding ingredients
    • C08K3/01—Use of inorganic substances as compounding ingredients characterized by their specific function
    • C08K3/013—Fillers, pigments or reinforcing additives
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L1/00—Compositions of cellulose, modified cellulose or cellulose derivatives
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L23/00—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
    • C08L23/02—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers not modified by chemical after-treatment
    • C08L23/04—Homopolymers or copolymers of ethene
    • C08L23/06—Polyethene
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L23/00—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
    • C08L23/02—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers not modified by chemical after-treatment
    • C08L23/04—Homopolymers or copolymers of ethene
    • C08L23/08—Copolymers of ethene
    • C08L23/0846—Copolymers of ethene with unsaturated hydrocarbons containing other atoms than carbon or hydrogen atoms
    • C08L23/0853—Vinylacetate
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L51/00—Compositions of graft polymers in which the grafted component is obtained by reactions only involving carbon-to-carbon unsaturated bonds; Compositions of derivatives of such polymers
    • C08L51/06—Compositions of graft polymers in which the grafted component is obtained by reactions only involving carbon-to-carbon unsaturated bonds; Compositions of derivatives of such polymers grafted on to homopolymers or copolymers of aliphatic hydrocarbons containing only one carbon-to-carbon double bond
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L9/00—Compositions of homopolymers or copolymers of conjugated diene hydrocarbons
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S273/00—Amusement devices: games
    • Y10S273/04—Ethylene
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S273/00—Amusement devices: games
    • Y10S273/05—Vinyl
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T428/00—Stock material or miscellaneous articles
    • Y10T428/13—Hollow or container type article [e.g., tube, vase, etc.]
    • Y10T428/1352—Polymer or resin containing [i.e., natural or synthetic]
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T428/00—Stock material or miscellaneous articles
    • Y10T428/13—Hollow or container type article [e.g., tube, vase, etc.]
    • Y10T428/1352—Polymer or resin containing [i.e., natural or synthetic]
    • Y10T428/1372—Randomly noninterengaged or randomly contacting fibers, filaments, particles, or flakes
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T428/00—Stock material or miscellaneous articles
    • Y10T428/13—Hollow or container type article [e.g., tube, vase, etc.]
    • Y10T428/1352—Polymer or resin containing [i.e., natural or synthetic]
    • Y10T428/1386—Natural or synthetic rubber or rubber-like compound containing

Definitions

  • This specification relates playballs, particularly tennis balls, and to ball manufacturing processes.
  • Gas filled rubber play balls for tennis and other games are well known. They contain gases at atmospheric pressure or at elevated pressures. Tennis balls filled with compressed gases are preferred by many players due to their perceived playing properties. Typically, the balls start out with gases at pressures of 10 psi (0.7 kg f/cm 2 , 0.069 MPa) above atmospheric pressure and then lose pressure during storage and use. The loss of pressure causes the playing characteristics of the ball to change.
  • pressurized balls balls with an internal pressure near atmospheric pressure. These are known as pressureless balls. To get playing characteristics similar to a pressurized ball, pressureless balls tend to have thicker walls than pressurized balls. To maintain the same ball weight with thicker walls, the density of the rubber compound in the wall needs to be lower.
  • thermoplastic polymeric fillers such as polystyrene
  • mineral type fillers because ofthe lower density of thermoplastics relative to many mineral type fillers.
  • the high melting temperatures of these thermoplastics require an extra processing step where the thermoplastics were blended with the elastomer and dispersed at the higher temperature where the thermoplastic softens.
  • a problem with many rubber ball compounds is the tendency of the ball to soften (the modulus of the cured ball decreases) as a result of the repeated deformation during play. This changes the play characteristics of the ball. A reduced tendency to soften is clearly an advantage.
  • EP-A-456036 describes making pressureless tennis balls using a rubber composition of one or more crosslinked rubbers, such as high cis-1,4 polybutadiene rubber, together with fillers which may be silica or cellulose powder.
  • EP-A-459436 describes pressureless tennis balls whose rubber composition contains 5 to 60 parts by weight of polyethylene per 100 parts by weight of rubber to improve rebound properties.
  • the present invention provides a playball in the form of a hollow sphere comprising a blend of at least:
  • the invention provides a method of making a playball as defined above, wherein the one or more rubbers, the one or more particulate fillers, and the polymeric filler/fillers are mixed together with one or more curatives to form a compounded blend, and the compounded blend is moulded into hollow ball halves; the adding and mixing of the aforementioned components being performed in an internal mixer prior to subjecting any of the resulting blends to a cooling step external to the mixer.
  • Reinforcing fillers used in various combinations are fine particle mineral type reinforcing fillers such as silica and/or carbon black, cellulose fibers, polyethylene and copolymers of ethylene vinyl acetate (EVA).
  • EVA ethylene vinyl acetate
  • An advantage of ethylene-vinyl acetate filler is that an extra step of removing the rubber compound from the mixer and cooling to a temperature lower than the activation temperature for the cure accelerators is not needed during the compounding of the rubber.
  • the polyethylene homopolymer is desirably grafted to the cellulose fibers.
  • the reinforcing fillers can optionally have surface treatments to enhance the elastomer-filler interactions. The substitution of skim rubber for a portion of natural rubber can increase the modulus and decrease the need for reinforcing fillers.
  • Play balls can be made by molding a compounded rubber blend. Molding can be accomplished by any conventional means such as compression, injection, transfer molding, etc.
  • the balls may be made as two hemispheres which are then adhesively joined to form a hollow sphere. They can optionally be formed with an internal gas under a pressure from about 6 to about 30 psig (0.04 to 0.2 MPa) above atmospheric pressure.
  • the preferred ball has an internal pressure from -3 or 0 to 5 psig (-0.02 or 0 to 0.034 MPa) above atmospheric pressure. Subsequently, it may be covered with a felt material to reduce wear and provide desirable play characteristics to a tennis ball.
  • the compounding can be performed on a two roll mill, Banbury, or other elastomer mixing equipment.
  • the compounded elastomer can be comprised of elastomeric rubbers; reinforcing mineral type fillers; other fillers; curatives, such as sulfur along with primary and secondary cure accelerators; processing aids; colorants; and protectorants.
  • the preferred play ball is a tennis ball meeting the specifications of the International Lawn Tennis Federation (ITF) which are:
  • tennis balls Prior to deflection measurements, tennis balls are preconditioned by compressing the balls to 25.4 mm (1 inch) deflection on each of the three orthogonal axes (x, y, z). All subsequent deflections are also measured along the three orthogonal directions.
  • the tennis ball In the first test to determine the deflection of the ball from rest (forward deformation or "forward deflection"), the tennis ball is compressed at a rate of 50.8 mm/min (2 inches/min) until a load of 1.36 kg (3 lbs.) is achieved, then the load is increased to 9.53 kg (21 lbs) providing a net load of 8.17 kg (18 lbs) and the resultant deflection is measured from the deflection at 1.36 kg load.
  • the average forward deflection may be from 5.59 to 7.37 mm (0.22 to 0.29 ins) (Earlier tolerances were from 6.73 to 7.37 mm).
  • a second test the deflection of the ball after a preliminary compression is measured.
  • the tennis ball is compressed with such force, while maintaining specific conditions, that the deflection is 25.4 mm (1 inch). Then the load is reduced to 9.53 kg (21 lbs.) and the deflection is measured. Then the load is reduced to 1.36 kg (3 lbs) and the deflection is measured again.
  • the reverse deflection is the difference in displacement of the ball at 9.53 kg load and the displacement at 1.36 kg load.
  • the displacement at 1.36 kg load is thus used as either a starting point or ending point for most displacement measurements by difference.
  • the average deflection that now results is greater on account of the greater previous compression of 25.4 mm (1 inch) which the ball is recovering from. This is called “reverse deflection" and, according to the regulations, must be between 8.89 and 10.8 mm (0.35 to 0.425 inch).
  • the elastomer portion of the ball is a highly resilient rubber.
  • Rubber is used to mean polymers that have rubbery properties. These include flexibility of the polymer backbone at the use temperature and the capability of being crosslinked.
  • the rubber can be at least one rubber and preferably blends of two or more rubbers. Preferred rubbers are polyisoprene types, polybutadiene (BR) of high 1,4-unit content, and skim rubber. Other diene containing polymers and copolymers such as styrene-butadiene rubbers can be incorporated.
  • the diene based copolymers can also be random copolymers, block copolymers, thermoplastic elastomers, graft copolymers, star polymers. Amounts of other compounding components will be stated per 100 parts by weight of the rubber (elastomer), abbreviated phr.
  • the molecular weights of the rubbers are desirably from about 50,000 to 500,000 or more.
  • the polyisoprene is desirably some form of natural rubber (NR) and/or synthetic high 1,4 content polyisoprene (i.e., >90%, desirably >95% 1,4-units and preferably about 100% cis 1,4 units). It is desirable as an option to include up to 100 phr, desirably up to 40 or 60, and preferably from 2 or 5 to 30 phr of skim rubber in the polyisoprene.
  • NR natural rubber
  • synthetic high 1,4 content polyisoprene i.e., >90%, desirably >95% 1,4-units and preferably about 100% cis 1,4 units. It is desirable as an option to include up to 100 phr, desirably up to 40 or 60, and preferably from 2 or 5 to 30 phr of skim rubber in the polyisoprene.
  • Skim rubber is a material which results from the production of natural rubber latex concentrate by centrifugation. After the centrifugation process, some 5-10% of the total rubber, together with an enhanced proportion of the non-rubber constituents of the original latex, remain in the serum phase. Coagulation of the solids in the serum phase by appropriate methods then gives "skim rubber.” Analyses indicate skim rubber can contain a hydrocarbon/rubber content of 75-85 wt. %, a protein content of 9.8-15.6 wt. %, a fatty acid content of 1.5-5.3 wt. %, acetone extractables besides fatty acids of 3-5 wt. %, and an ash content of 0.3-0.5 wt. %.
  • the polybutadiene has desirably at least 75 or 80%, preferably at least 98% of 1,4 units and desirably these are cis-1,4 units. Desirably, the 1,2 vinyl units are less than 20 or 25%, and preferably less than 18%.
  • the weight ratio of polyisoprene to polybutadiene is desirably from 100:0 to 0:100, desirably from 20:80 to 80:20, and preferably from 30:70 to 70:30, and most preferably from 50:50 to 65:35. Desirably, the 100 parts by weight rubber will be at least 90 wt. % and preferably 100 wt. % of said polyisoprene type rubber, said polybutadiene rubbers, and said skim rubber.
  • the fine particle size mineral type reinforcing fillers include silica and carbon black. These fillers can be distinguished from the polymeric fillers because the mineral type fillers have specific gravities of 1.2 and above and desirably from 1.6 to 2.0. Polymeric type fillers have specific gravities of 1.05 or less. Due to the tendency of carbon black to contaminate and discolor surrounding work areas, silica is preferred.
  • the fine particle reinforcing fillers can be used individually or as a blend at levels up to 40 phr, desirably 1 to 30 phr, and preferably from 5 to 20 phr.
  • the silica is desirably precipitated silica having median ultimate particle sizes of from about 0.01 to about 0.1, desirably from 0.02 to about 0.08, and preferably from 0.02 to about 0.04 ⁇ m. During precipitation, these small particles aggregate into larger structures.
  • Silicas include precipitated materials that are primarily SiO 2 but also include a blend of SiO 2 with metal oxides from aluminum and magnesium. Silicas of smaller particle size and higher structure are more effective at increasing modulus.
  • the silicas may optionally be surface treated, in the absence or presence of the rubber, to enhance their interaction with the elastomer.
  • Preferred surface treatments are mercaptosilanes having one or more hydrolyzable alkoxy groups on a silicon atom in the molecule, such as silanes of the structure (RO) 3 -Si-(CH 2 ) n -S 4 -(CH 2 ) n -Si(OR) 3 where n is from 1 to 5 and desirably n is 3, and R is a lower alkyl, HS(CH 2 ) 3 Si(OCH 3 ) 3 , or other silanes which are reactive both with the elastomers and the silica.
  • silanes of the structure (RO) 3 -Si-(CH 2 ) n -S 4 -(CH 2 ) n -Si(OR) 3 where n is from 1 to 5 and desirably n is 3, and R is a lower alkyl, HS(CH 2 ) 3 Si(OCH 3 ) 3 , or other silanes which are reactive both with the elastomers
  • Carbon blacks useful herein may have ASTM designations from N110 through N787.
  • the smaller sized particles with higher structure are more reinforcing than the larger sized particles.
  • the particle sizes can desirably range from 0.02 to about 0.10 ⁇ m.
  • Cellulose fibers with aspect ratios above 3 are desirable reinforcing agents. They may have a ribbon-shaped structure with an average thickness of 17 ⁇ m and an average length of from 290 ⁇ m to 760 ⁇ m. Cellulose with these dimensions as classified as fine, medium, and coarse. A preferred cellulose fiber is treated to aid dispersion with agents such as limestone or talc. One such product is CF Fibers from Custom Fibers International. Cellulose helps control ball rebound and forward deflection. It can be present up to about 30 phr, desirably from 1 to 25 phr, and preferably from about 10 to about 20 phr.
  • the cellulose fibers can be surface treated with resorcinol/formaldehyde bonding agents (such as Cohedur RL, supplied by Bayer) or by grafting reactions with polyethylene in the presence of a free radical source or with other surface modification.
  • resorcinol/formaldehyde bonding agents such as Cohedur RL, supplied by Bayer
  • EVA ethylene-vinyl acetate copolymers
  • crystalline does not imply total crystallinity but rather that the copolymer has crystalline regions therein. It has a lower crystalline melting temperature than polyethylene and can be blended with rubbers at normal processing temperatures and does not require a premixing step with the rubbers at elevated temperatures.
  • the EVA copolymer is desirably from 1 to 10, and preferably from 2 to 5 or 7 wt. % vinyl acetate and desirably from 90 to 99, and preferably from 93 or 95 to 98 wt. % polyethylene.
  • the softening point of the EVA copolymers is desirably from about 80 to 120°C, preferably about 85 to 115°C, and more preferably from 87 to 104°C.
  • the EVA polymer desirably has a molecular weight from about 50,000 to 2,000,000.
  • the EVA copolymer can be used in the compound from about 1 to about 30 phr, desirably from 5 to 25 phr, and preferably from 10 to 20 phr.
  • an ethylene-acrylic acid copolymer with from 1 to 10 wt. % acrylic acid and from 90 to 99 wt. % ethylene can be incorporated from about 1 to about 5 phr.
  • the molecular weight range for this polymer is the same as for the EVA.
  • thermoplastic ethylene vinyl acetate polymer avoids the mixing problems that occur with thermoplastics having higher melting temperatures or high Tg values. Since the EVA has a crystalline melting temperature, the polymer undergoes a dramatic change in modulus just above its melting point. Polyethylene and polymers high in styrene content need to be mixed with the rubbery polymers at a high temperature (such as above 115°, 120°, 130°, 140°, or 150°C) to achieve a good dispersion.
  • the accelerators used with the sulfur to cure the rubber are preferably not added to the rubbery polymers at these high temperatures as they can begin curing the rubbery polymers before molding. Rubber compounders are thus forced to use two or multiple pass mixing procedures when high temperatures are used for the initial mixing.
  • Two-pass mixing involves a first mixing operation (pass) at the recited higher temperatures where at least one of the rubbers and a thermoplastic are mixed, an intermediate cooling step (the rubbery compound can be sheeted off with a mill and cooled with air, water, or other heat transfer fluid), and a second mixing operation (pass) at a lower temperature during which heat sensitive components such as the accelerators are added. Therefore, it is desirable to exclude thermoplastic resins having a softening points that cannot be mixed in a single pass mix at temperatures of 120, 125, or 130°C or less. Such desirably excluded resins are low density polyethylene, linear low density polyethylene, other polyethylenes, and polymers with high styrene content.
  • An internal mixer is comprised of an enclosed mixing chamber or one capable of enclosure having at least one rotating shaft. Said at least one shaft being capable of exerting localized high shear stress to the material and being capable of exerting localized lower shear (homogenizing action) to polymer blends.
  • Examples of internal mixers include Banbury mixers, Bolling mixers and Shaw intermixers. These mixers are generally not capable of producing dramatic cooling rates during mixing operations. Consequently, cooling is usually accomplished on multiple roll mills.
  • EVA polymers proposed herein.
  • the low melt temperatures of EVA permit mixing them with the rubbers at temperatures sufficiently low (always at or below 120, 125, or 130°C) where the addition of curatives (sulfur and accelerators) is possible without the danger of premature curing.
  • a cooling step outside of the internal mixer is not necessary prior to adding the curatives.
  • a second mixing operation in the internal mixer is not needed. This saves equipment time, operator time, and minimizes the chance of errors by eliminating a step.
  • the use of prevulcanization inhibitors may allow higher mix temperatures for short periods of time after the accelerators are added.
  • One such inhibitor is N-(cyclohexlthio) phthalimide also known as SantogardTM PVI.
  • Polyethylene used as a reinforcing filler, can be prereacted with cellulose fibers in the presence of a free radical source, causing grafting of the polyethylene to the cellulose fibers.
  • the ethylene polymers or copolymers desirably have melting temperatures from 104°C to 190°C.
  • the polyethylene desirably has a molecular weight from about 50,000 to about 2,000,000.
  • the weight ratios of polyethylene to cellulose fibers can be from 90:10 to 10:90, desirably from 70:30 to 30:70, and preferably from 60:40 to 40:60.
  • the free radical sources include peroxides such as those formed from alkyls, aromatics, or alkyl substituted aromatics with from 3 to 12 carbon atoms per organo group; peresters; azo initiators such as AIBN; percarbonate initiators; and similar compounds. These reactions are desirably conducted in high shear rubber or plastic mixing equipment above the melting temperature of polyethylene or desirably from about 90°C to about 190°C and more desirably from 100°C to 130°C for time periods desirably from about 3 to about 30, and preferably from about 10 to about 20 minutes.
  • the amount of the reaction product of polyethylene grafted cellulose in the compounded rubber can be up to 50 phr, desirably from 5 to 40 phr, and preferably from 10 to 30 phr.
  • the ethylene-acrylic acid copolymer previously described can also be used in combination with the polyethylene and cellulose graft.
  • the compounded elastomer can contain other fillers at concentrations desirably up to 30, more desirably up to 20, and preferably from 5 to 15 phr. These include magnesium carbonate, zinc carbonate, barium sulfate, clays, talcs, soapstone, aluminum trihydrate, calcium carbonate, and related fillers. These fillers can also be treated with various silanes and other coupling agents such as previously disclosed (sizes) to enhance the properties of the filled elastomer.
  • the curatives can include sulfur from 0.5 to 6 phr, desirably from 1 to 5 phr; primary accelerators from 1.5 to 4, desirably from 2 to 3 phr such as thiazoles or sulfenamides; and secondary accelerators from 0.1 to 4.0, desirably from 1 to 2 phr such as thiurams, dithiocarbamates, and guanidines.
  • primary accelerators from 1.5 to 4
  • secondary accelerators from 0.1 to 4.0, desirably from 1 to 2 phr such as thiurams, dithiocarbamates, and guanidines.
  • secondary accelerators from 0.1 to 4.0, desirably from 1 to 2 phr such as thiurams, dithiocarbamates, and guanidines.
  • one primary and one secondary accelerator one could alter the amount and use either two primary or two secondary accelerators.
  • Zinc oxide and a fatty acid such as stearic acid are typically included in the compounded elastomer. These function to activate the cure and increase the extent of crosslink formation.
  • the preferred fatty acids have from 10 to 25 carbon atoms.
  • the compounded elastomer is compounded according to traditional elastomer mixing techniques as set out in texts such as "Rubber Technology" 3rd Edition, edited by Maurice Morton, Van Nostrand Reinhold: New York, 1987 , in chapter 2.
  • the compounded elastomer is then usually extruded into pellets (plugs) of sufficient weight to produce a hemispherical shell that is 1/2 of a ball.
  • Pellets can be compression molded in from about 2 to 5 minutes at from about 130 to 170°C and desirably from 140 to 160°C to form hollow hemispherical tennis ball halves.
  • the cure time used for molding halves in the examples was determined using a curemeter. The examples used the cure time to get 90% of the maximum torque.
  • the halves are then trimmed of the flash which holds the mat together and the edges are trimmed or buffed prior to adhesively joining the halves in a heated mold.
  • the adhesive is generally rubber based and sulfur cured with one or more accelerators.
  • the surface of the balls are then further buffed if a felt is to be applied.
  • Adhesive is applied to the ball and/or the felt edges and backing of the felt before the felt and ball are adhesively joined.
  • the felt typically has a dumbbell shape prior to application on the ball. Conventional tennis ball felts such as wool-nylon blends can be used.
  • the rubber compound has utility specifically for tennis balls, and more generally for play balls (assorted games where the ball is tossed bounced, and struck) which may be exercise balls (to be compressed or deformed as part of an exercise program).
  • a tennis ball should have a long life and consistent play behavior.
  • Ball softening is an undesirable increase in the forward deflection of the cured ball with repeated deformation.
  • a measure of ball softening that closely simulates repeatedly deforming a tennis ball with a tennis racquet is obtained with an air-powered cannon. The cannon propels balls at 24m/s (80 ft./sec.) against a stationary aluminium block.
  • the test apparatus is loaded with 8 balls and those balls are impacted 300 times in 10 minutes or approximately 37.5 times per ball in a ten minute period. At 10-minute intervals of time (0-80 min.), the balls are removed, tested for forward deflection and returned to the tester. Small changes in the measured forward deflection after a number of impacts correlates strongly with balls having superior resistance to softening during on-court play. Both tennis ball centers, felt, and ball adhesives are factors affecting ball softening.
  • a durability apparatus was used to measure the average time-to-failure (ATF). Failure is typically a rupture or catastrophic failure in the core.
  • the tester consists of an air-powered cannon which repeatedly impacts balls, against an aluminum block until a failure occurs. Eight balls are impacted successively 30 times per minute at an impact velocity average of 115 ft./sec. Testing of a given ball is stopped if the particular ball has not failed in 60 minutes. As a general rule, tennis balls with an ATF ⁇ 18 minutes provide good durability in play.
  • Ball No. 1 in Tables I and II shows the effect of cellulose modification on ball properties.
  • a composite of cellulose fibers grafted with a commercial low density polyethylene (Escorene LDPE) was prepared by free radical reaction involving 50 g cellulose fibers, 50 g LDPE, and 0.2 g dicumyl peroxide in a Banbury. About 12 minutes of mixing time was required for complete dispersion and grafting with the cellulose fibers. The initial Banbury temperature was 38°C while the final mix temperature was 177°C. A physical mixture of cellulose and LDPE was prepared similarly to the graft composite without the presence of dicumyl peroxide. This was used in comparative Ball 1R.
  • Pressureless tennis balls were fabricated from the rubber formulations shown in Table I.
  • the cellulose fibers grafted with LDPE as described above were formulated into Ball No. 1.
  • the results of ball property tests are shown with a comparative pressureless tennis ball (Ball No. 1R), based on a physical blend of LDPE and cellulose, and a competitive Ball No. 1C in Table II.
  • the results shown in Table II demonstrate the merit of modifying cellulose with LDPE in the presence of a free radical initiator. Particularly, a significant improvement in ball durability (during the air powered cannon average time-to-failure (ATF) test) was obtained while maintaining ball properties within or close to the realm of ITF specification.
  • the ATF of Ball No.1 is seen to be superior to the comparative Ball 1R and comparable to Competitive Ball No. 1C.
  • Ball No. 1C is considered to have outstanding durability based on laboratory and play test data.
  • the stress-strain properties of Ball No. 1 described herein are superior to the comparative Ball 1R and comparable to the Competitive Ball No. 1C.
  • the high values of tensile strength and elongation at break are an indication of the toughness of the Ball 1 centers and can be a predictor of on-court durability.
  • Ball No. 2 The effect of adding EVA to a tennis ball formulation is shown by Ball No. 2.
  • the exact recipe is in Table V, including 15 phr Escorene LD-302 (EVA, 3.5 wt. % vinyl acetate) and 7.5 phr Nucap 200 (a mercaptosilane coated aluminium silicate).
  • Table III shows the standard ball properties for Ball No. 2 using the EVA as proposed herein.
  • An ATF value of 30 is considered adequate for good durability for on-court play.
  • the balls were tested for ball softening using the air powered cannon for 80 minutes using the 24 m/s (80ft./sec) velocity.
  • the small "Increase in Deflection" shown in Table III for Ball No. 2 indicates good resistance to ball softening.
  • the formulation (Table V) for Ball No. 2R is taken from Example 1 of EP 0 459 436 Al with the use of a low density polyethylene (Escorene LD-138) as the polyethylene component. ZnCO 3 (10 phr) is incorporated to obtain ball weight consistent with ITF specifications.
  • the Shore D hardness (52) and flexural rigidity (2915) of the LD-138 are within the ranges of the polyethylenes A, B, C) disclosed in EP 0 459 436 Al, as shown in Table IV.
  • the flexural rigidity of the EVA copolymer is outside the ranges of the polyethylenes of EP 0 459 436 A1.
  • Ball No. 2 made using an EVA copolymer called LD-302 shown in Table VI, has higher rebound and lower deflection than the reference Ball No. 2R made using polyethylene called LD-138.
  • LD-302 is a copolymer of ethylene and vinyl acetate (EVA) having about 95-98% ethylene and 2-5 wt. % Vinyl acetate. It has a crystalline melting temperature (Tm) of about 87-104°C. Of greater significance is the substantially lower extent of ball softening ("Increase in Deflection") for Ball No. 2 vs. Ball No. 2R. These data predict a superior resistance to change in performance (ball softening) during on-court play, which is a desirable performance characteristic of tennis balls.
  • skim rubber The protein fraction in skim rubber is considered to provide enhanced reinforcement characteristics to vulcanisates. Skim rubber can reduce forward deflection in pressureless tennis balls without a significant loss in rebound. In addition, skim rubber can decrease ball deflection without a substantial weight penalty associated with the use of fillers such as silicas which have high specific gravities.
  • the data in Table VII show physical properties for Balls No. 3 and No. 3R.
  • the recipes for Balls No. 3 and 3R were similar to those in Table V.
  • Ball No. 3 substituted 20 phr skim NR and 40 phr SMR-GP (NR) and Ball No. 3R substituted 60 phr SMR-GP (NR) for 60 phr SMR-CV (NR) in Ball No. 2.
  • SMR-GP is a less expensive grade of natural rubber than SMR-CV.
  • Ball properties of pressureless tennis balls are compared in these compounds reinforced with EVA copolymer and silica.
  • Table VII the effect of replacing 33 wt. % of the natural rubber component (SMR-GP) with skim rubber in Ball No.
  • Ball No. 3 results in a reduction in forward deflection, as can be seen by comparing the data for Ball No. 3 versus Ball No. 3R.
  • Ball No. 3R is a reference ball identical to Ball No. 3 but without skim rubber. It is important to note in Table VII that the reduction in deflection occurs with an improvement in the resistance to ball softening without any significant change in rebound and average time-to-failure (ATF). Moreover, the substitution of skim rubber, a lower-cost type of NR, for SMR grades results in a lower-cost rubber compound. Comparison of Ball Properties of Ball No.3 with Reference Ball No. 3R Ball No. 3 Ball No.
  • Ball No.1 using blends of silica and the polyethylene grafted cellulose has enhanced durability over balls with polyethylene and cellulose.
  • Ball No. 2 has shown that an EVA copolymer with silica contributes to less ball softening during play than polyethylene.
  • Ball No. 3 has shown that skim rubber contributes to lower initial deflection without decreasing rebound and also results in less ball softening. but without skim rubber. It is important to note in Table X that the reduction in deflection occurs with an improvement in the resistance to ball softening (0.031 increase in deflection versus 0.041) without any significant change in rebound and average time-to-failure (ATF).
  • Ball No. 2 using blends of silica and the polyethylene grafted cellulose has enhanced durability over balls with polyethylene and cellulose.
  • Ball No. 3 has shown that an EVA copolymer with silica contributes to less ball softening during play than polyethylene.
  • Ball No. 8 has shown that skim rubber contributes to lower initial deflection without decreasing rebound and also results in less ball softening.

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  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • General Health & Medical Sciences (AREA)
  • Physical Education & Sports Medicine (AREA)
  • Compositions Of Macromolecular Compounds (AREA)

Claims (14)

  1. Balle de jeu sous la forme d'une sphère creuse comprenant un mélange d'au moins :
    (a) un ou plusieurs caoutchoucs réticulés, et
    (b) une Ou plusieurs charges particulaires de renforcement comprenant de la silice ou du noir de carbone ou leurs combinaisons,
       caractérisée par la présence dans le mélange de
    (c) une charge polymérique qui est (i) un copolymère d'éthylène-acétate de vinyle et/ou (ii) le produit réactionnel de la greffe de cellulose avec du polyéthylène en présence d'une source de radicaux libres.
  2. Balle de jeu selon la revendication 1, où le copolymère d'éthylène-acétate de vinyle est présent à raison de 5 à 30 phr et contient de 1 à 10 pour cent en poids d'acétate de vinyle et de 90 à 99 pour cent en poids d'éthylène.
  3. Balle de jeu selon la revendication 2, où le copolymère d'éthylène-acétate de vinyle contient 2 à 5 pour cent en poids d'acétate de vinyle et 95 à 98 pour cent en poids d'éthylène.
  4. Balle de jeu selon l'une quelconque des revendications 1 à 3, où le produit réactionnel de cellulose greffée de polyéthylène est présent en une quantité de 5 à 40 phr, le produit réactionnel ayant un rapport pondéral du polyéthylène à la cellulose de 10 :90 à 90 :10.
  5. Balle de jeu selon la revendication 4, où la cellulose a une structure en forme de ruban et a un revêtement de surface et où le rapport pondéral du polyéthylène à la cellulose est de 70 :30 à 30 :70.
  6. Balle de jeu selon l'une quelconque des revendications 1 à 5, où la cellulose a été greffée du pOlyéthylène en présence de la source de radicaux libres entre 90 et 190°C.
  7. Balle de jeu selon l'une quelconque des revendications 1 à 6 où la silice est présente en une quantité de 5 à 30 phr.
  8. Balle de jeu selon la revendication 7, où la silice a été traitée avec un mercaptosilane.
  9. Balle de jeu selon l'une quelconque des revendications 1 à 8, où ledit un ou plusieurs caoutchoucs comprend du polybutadiène avec au moins 75% d'unités 1,4, du polyisoprène avec au moins 90% d'unités 1,4, du caoutchouc écumé ou leurs combinaisons.
  10. Balle de jeu selon la revendication 9, où ledit un ou plusieurs caoutchoucs comprend du caoutchouc écumé en une quantité de 5 à 40 phr.
  11. Balle de jeu selon l'une quelconque des revendications 1 à 10, où :
    la balle de jeu a un recouvrement de feutre,
    la balle de jeu a un diamètre de 65,4 à 68,6 mm,
    la balle de jeu a un poids de 56,7 à 58,5 grammes, et
    la balle de jeu a une pression interne de l'ordre de -0,02 à +0,034 MPa relativement à la pression atmosphérique.
  12. Balle de jeu selon l'une quelconque des revendications 1 à 11, où la balle de jeu est une balle de tennis.
  13. Méthode de fabrication d'une balle de jeu selon l'une quelconque des revendications 1 à 12, où le ou les caoutchoucs, l'une ou les Charges particulaires et la ou les charges polymériques sont mélangés avec un ou plusieurs agents durcisseurs pour former un mélange malaxé et le mélange malaxé est moulé en moitiés de balle creuse ;
       l'addition et le mélange des composants ci-dessus mentionnés étant accomplis dans un mélangeur interne avant de soumettre tous les mélanges résultants à une étape de refroidissement externe au mélangeur.
  14. Méthode de fabrication d'une balle de jeu selon la revendication 13, où, pendant le mélange des composants, la température des mélanges et du mélange malaxé est toujours de 130°C ou moins.
EP94305731A 1993-08-05 1994-08-02 Balles de jeu, balles de tennis sans pression et compositions de caoutchouc pour les fabriques Expired - Lifetime EP0646396B1 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US102686 1993-08-05
US08/102,686 US5558325A (en) 1993-08-05 1993-08-05 Play balls or pressureless tennis balls

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EP0646396A2 EP0646396A2 (fr) 1995-04-05
EP0646396A3 EP0646396A3 (fr) 1995-08-09
EP0646396B1 true EP0646396B1 (fr) 1998-06-17

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US (1) US5558325A (fr)
EP (1) EP0646396B1 (fr)
JP (1) JP2610584B2 (fr)
CA (1) CA2128963C (fr)
DE (1) DE69411110T2 (fr)

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Also Published As

Publication number Publication date
DE69411110D1 (de) 1998-07-23
EP0646396A2 (fr) 1995-04-05
DE69411110T2 (de) 1998-12-24
AU6881294A (en) 1995-02-16
CA2128963A1 (fr) 1995-02-06
AU674417B2 (en) 1996-12-19
US5558325A (en) 1996-09-24
JPH07149958A (ja) 1995-06-13
EP0646396A3 (fr) 1995-08-09
JP2610584B2 (ja) 1997-05-14
CA2128963C (fr) 2001-07-03

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